SYSTEMS AND METHODS OF PRODUCING A CRUDE PRODUCT
Contact of a crude feed with one or more catalysts produces a total product that includes a crude product. The crude feed has a residue content of at least 0.2 grams of residue per gram of crude feed. The crude product is a liquid mixtur...

WO/2005/066309A2

SYSTEMS AND METHODS OF PRODUCING A CRUDE PRODUCT
Contact of a crude feed with one or more catalysts produces a total product that includes a crude product. The crude feed has a residue content of at least 0.2 grams of residue per gram of crude feed. The crude product is a liquid mixtur...

WO/2005/066302A2

SYSTEMS AND METHODS OF PRODUCING A CRUDE PRODUCT
Contact of a crude feed with one or more catalysts produces a total product that includes a crude product. The crude feed has a residue content of at least 0.2 grams of residue per gram of crude feed. The crude product is a liquid mixtur...

WO/2005/066305A2

SYSTEMS AND METHODS OF PRODUCING A CRUDE PRODUCT
Contact of a crude feed with one or more catalysts produces a total product that includes a crude product. The crude feed has a residue content of at least 0.2 grams of residue per gram of crude feed. The crude product is a liquid mixtur...

WO/2005/066316A2

SYSTEMS AND METHODS OF PRODUCING A CRUDE PRODUCT
Contact of a crude feed with one or more catalysts produces a total product that includes a crude product. The crude feed has a residue content of at least 0.2 grams of residue per gram of crude feed. The crude product is a liquid mixtur...

WO/2005/066304A2

SYSTEMS AND METHODS OF PRODUCING A CRUDE PRODUCT
Contact of a crude feed with one or more catalysts produces a total product that includes a crude product. The crude feed has a residue content of at least 0.2 grams of residue per gram of crude feed. The crude product is a liquid mixtur...

WO/2005/063936A2

SYSTEMS AND METHODS OF PRODUCING A CRUDE PRODUCT
Contact of a crude feed with one or more catalysts produces a total product that includes a crude product. The crude feed has a residue content of at least 0.2 grams of residue per gram of crude feed. The crude product is a liquid mixtur...

WO/2005/063675A2

SYSTEMS AND METHODS OF PRODUCING A CRUDE PRODUCT
Contact of a crude feed with one or more catalysts produces a total product that includes a crude product. The crude feed has a residue content of at least 0.2 grams of residue per gram of crude feed. The crude product is a liquid mixtur...

WO/2005/063928A2

SYSTEMS AND METHODS OF PRODUCING A CRUDE PRODUCT
Contact of a crude feed with one or more catalysts produces a total product that includes a crude product. The crude feed has a residue content of at least 0.2 grams of residue per gram of crude feed. The crude product is a liquid mixtur...

WO/2005/063932A2

SYSTEMS AND METHODS OF PRODUCING A CRUDE PRODUCT
Contact of a crude feed with one or more catalysts produces a total product that includes a crude product. The crude feed has a residue content of at least 0.2 grams of residue per gram of crude feed. The crude product is a liquid mixtur...

WO/2005/061665A2

SYSTEMS AND METHODS OF PRODUCING A CRUDE PRODUCT
Contact of a crude feed with one or more catalysts produces a total product that includes a crude product. The crude feed has a residue content of at least 0.2 grams of residue per gram of crude feed. The crude product is a liquid mixtur...

WO/2005/061664A2

SYSTEMS AND METHODS OF PRODUCING A CRUDE PRODUCT
Contact of a crude feed with one or more catalysts produces a total product that includes a crude product. The crude feed has a residue content of at least 0.2 grams of residue per gram of crude feed. The crude product is a liquid mixtur...

WO/2005/061671A2

SYSTEMS AND METHODS OF PRODUCING A CRUDE PRODUCT
Contact of a crude feed with one or more catalysts produces a total product that includes a crude product. The crude feed has a residue content of at least 0.2 grams of residue per gram of crude feed. The crude product is a liquid mixtur...

WO/2005/061676A1

METHOD OF HYDROGENATION OF HEAVY OIL
A method of hydrogenation of heavy oil. A first step involves providing a continuous pipe reactor defining a serpentine flow path. A second step involves heating heavy oil to lower the viscosity of the heavy oil. A third step involves pu...

"CRYSTALLINE ALUMINOSILICATE ZEOLITIC COMPOSITION: UZM-4M"
A crystalline aluminosilicate zeolite identified as UZM-4M has been synthesized. This zeolite is obtained by treating a UZM-4 zeolite with a fluorosilicate salt to obtain a zeolite having the empirical formula:M1an+Al1-xExSiyOzwhere M1 i...

TITANIA SUPPORTS FOR FISHER-TROPSCH CATALYSTS
Shaped catalyst carrier containing titania, wherein at least 50 wt% of the titania is present as brookite, and wherein the carrier comprises between 40 and 100 wt% of crystalline titania based on the total weight of the carrier. Catalyst...

METHOD OF STARTING UP A REACTION SYSTEM
The invention is directed to methods of starting up reaction systems. The reaction systems are those that use catalysts that comprise molecular sieves, particularly metalloaluminophosphate molecular sieves, especially metalloaluminophosp...

WO/2005/019389A1

METHOD OF SHUTTING DOWN A REACTION SYSTEM
The invention is directed to methods of shutting down reaction systems. The reaction systems are those that use catalysts that comprise molecular sieves, particularly metalloaluminophosphate molecular sieves, especially metalloaluminopho...

WO/2005/019382A2

CATALYTIC DISTILLATION HYDROPROCESSING
A method for hydroprocessing a hydrocarbon synthesis product feed to form upgraded fuels and lubricating oils. In a preferred embodiment, the method includes the steps of: (a) contacting a Fischer-Tropsch product with a hydroprocessing c...

ALKYLATION OF PARAFFINS WITH OLEFINS
A process for the alkylation of paraffins with olefins includes contacting the paraffin with the olefin under alkylation conditions with a zeolite having an AAI number of at least about 1.0. In a preferred process isobutane is alkylated ...

WO/2005/007776A1

METHOD FOR PRODUCTION AND UPGRADING OF OIL
An integrated process for production and upgrading of heavy and extra-heavy crude oil, comprising (a) reforming of hydrocarbons such as natural gas to produce hydrogen, CO2 and steam (b) separating the produced hydrogen from the CO2, ste...

WO/2005/005575A1

PROCESS TO PREPARE A FISCHER-TROPSCH PRODUCT
Process to prepare a waxy Raffinate product by performing the following steps: (a) subjecting a Fischer-Tropsch derived product having a weight ratio of compounds boiling above 540°C and compounds boiling between 370 and 540°C of great...

HYDROCARBON CONVERSION PROCESS AND CATALYST
A process for hydrocracking a hydrocarbonaceous feedstock into a middle distillate utilising a hydrocarbon conversion catalyst comprising a modified beta zeolite and a modified Y zeolite, an amorphous inorganic oxide and a hydrogenation ...

WO/2005/000998A1

A CRACKING CATALYST WITH DESULFURIZATION
The present invention relates to a composition with desulfurization, in which molecular sieves of vanadium on its framework act as desulfarized element. The above composition process such features as high thermal stability and low vanadi...